Method for manufacturing  calcium silicate based composition

ABSTRACT

Provided is a method that enables a calcium silicate-based material to be produced more efficiently. The method of producing a calcium silicate-based material comprises: ( 1 ) a step of obtaining a reaction product by reacting raw materials containing a calcium component, a silicon component and an aluminum component in an aqueous medium; and ( 2 ) a step of forming calcium silicate by subjecting the reaction product to hydrothermal treatment.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to a novel method of producing a calciumsilicate-based material.

2. Description of the Related Art

Calcium silicate is used in various applications, including not onlypharmaceuticals and food additives, but also molding assistants andinsulating materials. A known example of a typical production method ofcalcium silicate is a production method of calcium silicate or a calciumsilicate-gypsum complex including a reaction step of mixing and reactinggypsum and an alkaline silicate in an aqueous medium, a washing step ofwashing a solid fraction obtained in the reaction step, a slurry step ofconverting the solid fraction obtained in the washing step to a slurry,a hydrothermal treatment step of carrying out hydrothermal treatment onthe slurry solution obtained in the slurry step, and a separation stepof separating the calcium silicate or calcium silicate-gypsum complexobtained in the hydrothermal treatment step (Japanese Patent ApplicationPublication No. S56-5317). Other methods for producing calcium silicateaccording to various conditions have also been proposed (Japanese PatentApplication publication Nos. S55-85445, S55-32753 and S54-93698).

Since calcium silicate produced by a method like that described abovehas particularly large bulk specific volume and oil absorption, it canbe used, for example, as an additive for preventing adhesion orimproving fluidity of dehumidifying agents, a carrier for impregnating aliquid substance and the like, a molding assistant or an adsorbent. Inparticular, calcium silicate has been proposed for used in theformulation of pharmaceuticals due to its specific aspect ratio and highoil absorption (Japanese Patent No. 4431391).

However, there is still room for improvement of conventional methodsused to produce calcium silicate with respect to conditions of thehydrothermal synthesis reaction (and particularly, with respect to thetemperature and duration thereof). Namely, although being able tosynthesize calcium silicate in a shorter period of time and at a lowertemperature would make it possible to contribute to production on anindustrial scale, such technology has yet to be developed.

SUMMARY OF THE INVENTION

Thus, a primary object of the present invention is to provide a methodthat enables a calcium silicate-based material to be produced moreefficiently. In addition, another object of the present invention is toprovide a calcium silicate-based material having high levels of bulkspecific volume and oil absorption.

As a result of conducting extensive studies in consideration of theproblems of the related art, the inventors of the present inventionfound that the above-mentioned objects can be achieved by employing aspecific method, thereby leading to completion of the present invention.

Namely, the present invention relates to a production method of acalcium silicate-based material as described below.

1. A method of producing a calcium silicate-based material, comprising:

(1) a step of obtaining a reaction product by reacting raw materialscontaining a calcium component, a silicon component and an aluminumcomponent in an aqueous medium; and

(2) a step of forming calcium silicate by subjecting the reactionproduct to hydrothermal treatment.

2. The production method described in 1 above, wherein at least one typeof aluminum compound selected from the group consisting of an aluminumsalt, an aluminum hydroxide and an aluminum oxide is used for a supplysource of the aluminum component.3. The production method described in 2 above, wherein the aluminumcompound is at least one type selected from the group consisting ofsodium aluminate, aluminum chloride and aluminum hydroxide.4. The production method described in 1 above, wherein the calciumsilicate contains gyrolite calcium silicate crystals.5. The production method described in 1 above, wherein the molar ratioof Al₂O₃/SiO₂ in the raw materials is 0.002 or more.6. The production method described in 1 above, wherein the hydrothermaltreatment is performed under conditions of a temperature of 150° C. to250° C. and a time of 1 to 4 hours.7. A calcium silicate-based material containing an aluminum component,wherein the calcium silicate-based material has:

(1) a bulk specific volume of 3 mL/g or more and an oil absorption of2.5 mL/g or more; and

(2) an aluminum content of 0.1% by weight to 1.0% by weight.

8. The calcium silicate-based material described in 7 above, whichcontains gyrolite calcium silicate crystals.9. The calcium silicate-based material described in 7 above, wherein thespecific surface area is 120 m²/g or more.10. A pharmaceutical composition including the calcium silicate-basedmaterial described in 7 above.

ADVANTAGES OF THE INVENTION

According to the production method of a calcium silicate-based materialof the present invention, a calcium silicate-based material can beefficiently produced by adding an aluminum component to the rawmaterials. In particular, calcium silicate-based material having highlevels of bulk specific volume and oil absorption can be produced at alower temperature and/or in a shorter period of time in a hydrothermaltreatment step.

The calcium silicate-based material of the present invention has higherlevels of bulk specific volume and oil absorption. In addition, specificsurface area is also comparatively large. Consequently, the calciumsilicate-based material of the present invention can be used in variousapplications as indicated below by taking advantage of thesecharacteristics.

(1) Adhesion Prevention and Fluidity Improvement of Dehumidifying Agents

The calcium silicate-based material of the present invention can be usedto produce composite particles such as calcium chloride by utilizing thehigh liquid absorption and moldability thereof. In this case sincemoisture absorbed by calcium chloride can be incorporated in the calciumsilicate-based material, there is hardly any wetting of the particlesurfaces and it is possible to maintain a dry state.

(2) Carrier Impregnation of Liquid Substances

In the case of impregnating a liquid such as a fragrance into a formedbody (including granules) of the calcium silicate-based material of thepresent invention, the fragrance and the like can be sustained for along period of time due to the large amount of liquid absorbed.

(3) Conversion of Liquids to Powders

Since the calcium silicate-based material of the present invention has acomparatively large pore volume, it is suitable for use in convertingliquids having a high viscosity in particular to a powder. For example,it can be preferably used to convert not only the previously describedliquid fragrance, but also liquid nutrient agents (such a vitamin E) orliquid antistatic agents and the like to powders.

(4) Molding Assistant

The calcium silicate-based material of the present invention can bepreferably used as a molding assistant in the production of granules ofsolid bath agents or adsorbents and the like.

(5) Various Additives

The calcium silicate-based material of the present invention can be usedas a carrier for solidifying liquid substances such as vitamins andother liposoluble drugs or liquid substances obtained by dissolvingsolid drugs. In addition, the calcium silicate-based material of thepresent invention can be used as a controlled-release additive (vehicle)for controlling the release (release rate) of an active ingredient, aswell as a fluidity improver, pH adjuster or stabilizer and the like.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a drawing showing an example of the steps of the productionmethod of the present invention;

FIG. 2 is a graph showing the results of investigating the effects of anadded amount of an aluminum component on bulk specific volume and oilabsorption; and

FIG. 3 is a graph showing the results of investigating the effects of anadded amount of an aluminum component on bulk specific volume and oilabsorption.

DESCRIPTION OF THE PREFERRED EMBODIMENTS 1. Production Method of CalciumSilicate-Based Material

The production method of a calcium silicate-based material of thepresent invention comprises:

(1) a step of obtaining a reaction product by reacting raw materialscontaining a calcium component, a silicon component and an aluminumcomponent in an aqueous medium (reaction step); and

(2) a step of forming calcium silicate by subjecting the reactionproduct to hydrothermal treatment (hydrothermal treatment step).

Reaction Step

In the reaction step, a reaction product is obtained by reacting rawmaterials containing a calcium component, a silicon component and analuminum component in an aqueous medium.

At least one type of aqueous medium selected from the group consistingof water and a water-soluble organic solvent can be used for the aqueousmedium. Examples of water-soluble organic solvents that can be usedinclude alcohol such as methanol, ethanol or propanol, and acetone orthe like. In the present invention, water is used particularlypreferably. There are no particular limitations on the amount of waterused, and normally the amount of water used is suitably adjusted so thatthe solid fraction concentration of the raw materials is about 1% byweight to 25% by weight.

The raw materials consist of a calcium component, a silicon componentand an aluminum component. Compounds serving as supply sources of thesecomponents can be used for each component.

A calcium compound serving as a supply source of the calcium componentcan be used for the calcium component. Examples of calcium compoundsthat can be used include calcium salts, calcium hydroxides and calciumoxides. Calcium salts such as calcium salts such as sulfates, chlorides,nitrates, carbonates or phosphates of calcium can be used particularlypreferably. Specific examples thereof include calcium sulfate (orgypsum) and calcium chloride. In the present invention, water-solublecalcium compounds are used preferably.

A silicon compound serving as a supply source of the silicon componentcan be used for the silicon component. Examples of silicon compoundsthat can be used preferably include silicates such as sodium silicate orpotassium silicate. In the present invention, water-soluble siliconcompounds are used preferably.

An aluminum compound serving as a supply source of the aluminumcomponent can be used for the aluminum component. Examples of thealuminum compounds include at least one type selected from the groupconsisting of aluminum salts, aluminum hydroxides and aluminum oxides.More specifically, at least one type of aluminum compound selected fromthe group consisting of sodium aluminate, aluminum chloride and aluminumhydroxide can be used preferably.

The blending ratio of the raw materials with respect to the calciumcomponent and silicon component in particular is such that the resultingcomposition thereof is represented by calcium silicate(2CaO.3SiO₅.mSiO₂.nH2O (wherein, 1≦m≦2, 2≦n≦3)). Thus, the molar ratioof Ca/Si is preferably set within the range of about 0.4 to 0.5.

With respect to the aluminum component, the molar ratio of Al₂O₃/SiO₂ inthe raw materials is preferably 0.002 or more, and in particular, theraw materials are more preferably blended so that the above-mentionedmolar ratio is 0.003 or more. Furthermore, although the upper limit ofthe above-mentioned Al₂O₃/SiO₂ molar ratio can be suitably setcorresponding to the application of the calcium silicate and the like,it is normally about 0.04.

An additive in the form of a pH adjuster (such as sodium hydroxide) canbe suitably incorporated in the raw materials as necessary.

The raw materials added in the prescribed blending ratios are mixed inan aqueous medium and allowed to react. Although the reactiontemperature in this case is not limiting, it is preferably set to, forexample, 5° C. to 100° C., and particularly to within the range of 5° C.to 25° C. The reaction time can be suitably adjusted corresponding tothe reaction temperature and the like. A reaction product can beobtained from the above-mentioned raw materials in this manner.

The resulting reaction product can also be rinsed with water prior tohydrothermal treatment as necessary. A method similar to a known methodmay be used to rinse (wash) the reaction product, and for example, amethod can be employed in which the reaction product is subjected tosolid-liquid separation followed by rinsing with water. The method usedfor solid-liquid separation is not limiting, and a known method such asfiltration or centrifugal separation may be used. The above-mentionedrinsing can also be carried out repeatedly.

Hydrothermal Treatment Step

In the hydrothermal treatment step, calcium silicate (and particularly,crystalline calcium silicate) is prepared by subjecting theabove-mentioned reaction product to hydrothermal treatment.

An aqueous medium may be added to the reaction product to form a slurryat the time of hydrothermal treatment. An aqueous medium such as any ofthe previously exemplified aqueous media can be used for the aqueousmedium in this case. Although there are no particular limitations on thesolid fraction concentration of the slurry, it is normally 1% by weightto 15% by weight and preferably about 3% by weight to 10% by weight.

Hydrothermal treatment can be carried out using a known device such asan autoclave. The reaction temperature is normally within the range of150° C. to 250° C. The duration of hydrothermal treatment is an amountof time that is adequate for forming the prescribed crystalline calciumsilicate. With respect to the temperature and time of the hydrothermaltreatment in the present invention, by incorporating an aluminumcomponent in the raw materials, a calcium silicate-based material havinghigh bulk specific volume and oil absorption can be prepared at a lowertemperature and in a shorter period of time. In other words, reacting atthe same temperature for the same amount of time allows the obtaining ofa calcium silicate-based material having higher levels of bulk specificvolume and oil absorption.

2. Calcium Silicate-Based Material

The present invention also includes a calcium silicate-based materialcontaining an aluminum component, wherein the calcium silicate-basedmaterial has:

(1) a bulk specific volume of 8 mL/g or more and an oil absorption of2.5 mL/g or more; and

(2) an aluminum content of 0.1% by weight to 1.0% by weight. A calciumsilicate-based material obtained according to the production method ofthe present invention in particular can be used preferably for this typeof calcium silicate-based material.

The calcium silicate-based material of the present invention has bulkspecific volume of 8 mL/g or more and preferably 10 mL/g or more. Inaddition, the calcium silicate-based material of the present inventionhas oil absorption of 2.5 mL/g or more and preferably 2.5 mL/g or more.

The calcium silicate-based material of the present invention containscalcium silicate and an aluminum component, and is substantiallypreferably composed of calcium silicate and an aluminum componentcontaining in calcium silicate.

Although the content of aluminum in the calcium silicate-based materialcan be suitably set corresponding to the application or usage method andthe like of the calcium silicate, it is normally 0.1% by weight or moreand preferably 0.2% by weight or more. Furthermore, the upper limit ofthe aluminum content is about 1.0% by weight.

The calcium silicate-based material of the present invention containscalcium silicate crystals, and more preferably contains gyrolite calciumsilicate crystals. Gyrolite calcium silicate crystals in particular arecomposed of rose flower petal-shaped particles formed by aggregation ofthin flakes, thereby making it possible to achieve the desired levels ofbulk specific volume and oil absorption.

The calcium silicate-based material of the present invention is normallyin the form of a powder, and the average particle diameter thereof iswithin the range of 1 μm to 100 μm and preferably within the range of 10μm to 40 μm.

Although there are no particular limitations on the specific surfacearea of the calcium silicate-based material of the present invention, itis preferably 120 m²/g or more, more preferably 120 m²/g to 200 m²/g andmost preferably 120 m²/g to 180 m²/g. Specific surface area of thepresent invention indicates a value obtained by measuring 0.02 g sampleof a powder of the calcium silicate-based material of the presentinvention according to the multipoint BET method using the measuringdevice and under the pretreatment and test conditions indicated below.

Measuring device: High-speed specific surface area and pore sizedistribution measuring device (NOVA-4000e, Quantachrome Corp.)

Pretreatment conditions: Holding for 1 hour at 105° C. while degassing

Test conditions: Measuring with the 3-point plot method according to thenitrogen adsorption method (relative pressure: 0.1, 0.2, 0.3)

The pH (5% SUS) of the calcium silicate-based material of the presentinvention is normally alkaline, and more particularly, is 8 or higherand preferably 8.5 to 9.5. The pH in this case is the value obtained bymeasuring the pH of a liquid in which 2.5 g of sample are suspended in50 mL of water with a pH meter.

The calcium silicate-based material of the present invention ischaracterized by having comparatively large pores in the case thecalcium silicate is substantially composed of flower petal-shapedgyrolite calcium silicate crystals as previously described. As a result,differing from pores formed between aggregated particles of amorphoussilicic anhydride, the calcium silicate-based material of the presentinvention is able to demonstrate high levels of liquid absorption orliquid retention properties and the like. For example, even in the caseof having compression molded the calcium silicate-based material of thepresent invention into tablets, as a result of having large pores asdescribed above, the resulting tablets are able to demonstrate highlevels of liquid absorption or liquid retention properties and the like.The mean pore size of such a structure is normally about 6 nm to 100 nm.In addition, the pore volume is about 0.1 cc/g to 6.0 cc/g.

3. Pharmaceutical Composition

The present invention also includes a pharmaceutical compositioncontaining the calcium silicate-based material of the present invention.The calcium silicate-based material of the present invention can be usednot only as, for example, a vehicle, molding assistant or stabilizer,but also as a carrier of a liquid substance obtained by dissolving aliquid drug or solid drug. Thus, the calcium silicate-based material ofthe present invention can be used preferably in the case of formulatinginto tablets, for example. In addition, by loading an active ingredientinto the pores of the calcium silicate-based material of the presentinvention, elution and gradual release of the active ingredient can bearbitrarily controlled.

There are no particular limitations on active ingredients(pharmaceutically active ingredients) that can be used in thepharmaceutical composition of the present invention, and any known orcommercially available active ingredient can be used. Examples of activeingredients that can be used include hyperlipemia drugs, antiulcerdrugs, antihypertensive drugs, antidepressants, antiasthnmatic drugs,antiepileptic drugs, antiallergic drugs, antibacterial drugs, anticancerdrugs, analgesics, anti-inflammatory drugs, antidiabetic drugs,antimetabolites, antagonists, osteoporosis drugs, antiplatelet drugs,antiemetic drugs, anesthetic drugs and hormone preparations.

Although the content of the calcium silicate-based material in thepharmaceutical composition of the present invention is not limiting, itcan normally be suitably adjusted to within the range of 0.1% by weightto 99% by weight.

In addition, in the pharmaceutical composition of the present invention,a known pharmaceutical additive may also be contained in addition to theabove-mentioned calcium silicate-based material and pharmaceuticallyactive ingredient. Examples of pharmaceutical additives that can be usedinclude excipients (such as lactose), disintegration agents (such ascrospovidone or lowly substituted hydroxypropyl cellulose (L-HPC)),binders (such as methyl cellulose, ethyl cellulose, hydroxypropylcellulose or hydroxypropyl cellulose), lubricants (such as magnesiumstearate or calcium stearate), pH adjusters (such as citric acid, aceticacid, sulfuric acid, hydrochloric acid, lactic acid, sodium hydroxide orpotassium hydroxide) and stabilizers (such as magnesium hydroxide,magnesium carbonate, magnesium oxide, calcium hydroxide, calciumcarbonate, calcium oxide, hydrotalcite or hydrated silicon dioxide,magnesium aluminate metasilicate, magnesium silicate, calcium phosphateor calcium hydrogen phosphate). Although there are no particularlimitations on the content of pharmaceutical additives provided it iswithin a range that does not impair the effects of the presentinvention, normally the content of pharmaceutical additives ispreferably within the range of 0.1% by weight to 99% by weight.

The pharmaceutical composition can be applied in various drug forms. Forexample, the pharmaceutical composition may be in the form of a tablet,powder, capsule, granule, suspension or emulsion.

EXAMPLES

The following provides a more detailed explanation of characteristics ofthe present invention by indicating examples and comparative examplesthereof. However, the scope of the present invention is not limited tothe examples.

Example 1

A calcium silicate-based material was prepared according to theproduction flow shown in FIG. 1. First, 0.5 kg of gypsum dihydrate and6.79 kg of water were placed in a reaction tank followed by stirringwell to prepare a slurry. Next, 1.303 kg of JIS-3 sodium silicate andprescribed amounts of additives shown in sample nos. 2 to 6 and 9 to 11of Table 1 (aluminum compound and sodium hydroxide) were added whilestirring the slurry, followed by allowing to react while mixing the rawmaterials under atmospheric pressure at 20° C. to 25° C. (reactionstep). The molar ratio of CaSO₄/Na₂O.nSiO; charged at this time was1.06. Next, after filtering the reaction product, the reaction productwas washed using water (washing step). Water was added to the resultingcake to prepare a slurry having a solid content of 5% by weight. Thisslurry was placed in an autoclave followed by carrying out hydrothermaltreatment at the temperatures and times indicated in Table 1 with theautoclave sealed (hydrothermal treatment step). Following completion ofhydrothermal treatment, the treated slurry was filtered and theresulting solid was dried for 24 hours at 105° C. (drying step).Powdered calcium silicate-based materials (sample nos. 2 to 6 and 9 to11) were obtained in this manner.

As a result of analyzing the resulting samples by X-ray diffraction, allof the samples were confirmed to gyrolite calcium silicate. In addition,as a result of observing the samples with a scanning electronmicroscope, all of the samples were confirmed to be in the form offlower petals.

Comparative Example 1

A calcium silicate-based material was prepared according to theproduction flow shown in FIG. 1. First, 0.5 kg of gypsum dihydrate and6.79 kg of water were placed in a reaction tank followed by stirringwell to prepare a slurry. Next, 1.303 kg of JIS-3 sodium silicate andprescribed amounts of additives (aluminum compound and sodium hydroxide)shown in Table 1 (sample nos. 1, 7 and 8) were added while stirring theslurry, followed by allowing to react while mixing the raw materialsunder atmospheric pressure at 20° C. to 25° C. (reaction step). Themolar ratio of CaSO₄/Na₂O.nSiO₂ charged at this time was 1.06. Next,after filtering the reaction product, the reaction product was washedusing water (washing step).

Water was added to the resulting cake to prepare a slurry having a solidcontent of 5% by weight. This slurry was placed in an autoclave followedby carrying out hydrothermal treatment at the temperatures and timesindicated in Table 1 with the autoclave sealed (hydrothermal treatmentstep). Following completion of hydrothermal treatment, the treatedslurry was filtered and the resulting solid was dried for 24 hours at105° C. (drying step). Powdered calcium silicate-based materials (samplenos. 1, 7 and 8) were obtained in this manner.

Comparative Example 2

0.5 kg of gypsum dihydrate and 6.79 kg of water were placed in areaction tank followed by stirring well to prepare a slurry. Next, 1.303kg of JIS-3 sodium silicate and a prescribed amount of sodium hydroxideshown in Table 1 (sample no. 12) were added while stirring the slurry,followed by allowing to react while mixing the raw materials underatmospheric pressure at 20° C. to 25° C. (reaction step). The molarratio of CaSO₄/Na₂O.nSiO charged at this time was 1.06. Next, afterfiltering the reaction product, the reaction product was washed usingwater (washing step). Water was added to the resulting cake followed bythe addition of 0.010 kg of aluminum hydroxide to prepare a slurryhaving a solid content of 5% by weight. This slurry was placed in anautoclave followed by carrying out hydrothermal treatment at thetemperatures and times indicated in Table 1 with the autoclave sealed(hydrothermal treatment step). Following completion of hydrothermaltreatment, the treated slurry was filtered and the resulting solid wasdried for 24 hours at 105° C. (drying step). A powdered calciumsilicate-based material (sample no. 12) was obtained in this manner.

TABLE 1 Raw Materials Physical JIS-3 Additives Hydrothermal Propertiessodium Gypsum Na aluminate, Treatment Oil silicate dihydrate Water Nahydroxide Temp. Time Bulk absorption No. (kg) (kg) (kg) (kg) Al (%) (°C.) (h) (ml/g) (ml/g) 1 1.303 0.5 6.79 Al—Na* 0 0.0058% 200 3 7.35 2.5NaOH 0.127 2 1.303 0.5 6.79 Al—Na 0.010 0.10% 200 3 11.77 3.4 NaOH 0.1223 1.303 0.5 6.79 Al—Na 0.014 0.15% 200 3 12.15 3.4 NaOH 0.120 4 1.3030.5 6.79 Al—Na 0.019 0.19% 200 3 12.99 2.9 NaOH 0.117 5 1.303 0.5 6.79Al—Na 0.029 0.38% 200 3 15.39 3.6 NaOH 0.112 6 1.303 0.5 6.79 Al—Na0.049 0.60% 200 3 15.00 3.4 NaOH 0.096 7 1.303 0.5 6.79 Al—Na 0.096 1.4%200 3 5.7 2.5 NaOH 0.056 8 1.303 0.5 6.79 Al—Na 0 0.01% 200 4 8.6 4.6NaOH 0.127 9 1.303 0.5 6.79 Al—Na 0.029 0.23% 200 4 14.3 5.0 NaOH 0.11210 1.303 0.5 6.79 AlOH 0.010 0.4% 200 3 13.5 3.6 NaOH 0.127 11 1.303 0.56.79 Al chloride 0.1% 200 3 10.8 3.6 hexahydrate 0.031 NaOH 0.127 121.303 0.5 6.79 AlOH 0.010 0.13% 200 3 8.8 2.1 (added after washing) NaOH0.127 *Al—Na represents sodium aluminate.

Test Example 1

Each of the samples obtained in the above-mentioned examples andcomparative examples were measured for aluminum content, bulk specificvolume and oil absorption. The results are shown in Table 1.Furthermore, measurement of aluminum content, bulk specific volume andoil absorption were carried out as described below.

(1) Aluminum Content

Aluminum content was measured according to the standard addition methodusing the measuring device and under the measuring conditions indicatedbelow.

1.0 g of sample were accurately weighed followed by the addition of 30mL of dilute hydrochloric acid, heating for 1 hour over a water bath,cooling and brining to a volume of 100 mL with ultrapure water. Theliquid was filtered with quantitative filter paper (No. 5C) and thefiltrate was used as a test solution. This test solution was measuredfor aluminum content according to the standard addition method using anICP optical emission spectrometer.

Measuring device: Vista-PRO (Seiko Instruments Inc.)

Measuring conditions: Atmospheric argon-nitrogen

-   -   Internal standard Y    -   Al 396.152    -   Y 377.433

(2) Bulk Specific Volume

2.5 g of sample were weighed out and placed in a 50 mL graduatedcylinder followed by tapping from a height of 4 cm at a rate of 100times/250 seconds, measuring the volume of the powder and calculatingbulk specific volume according to the equation shown below.

Bulk specific volume (mL/g)=Powder volume (mL)/powder weight (g)

(3) Oil Absorption

1.0 g of sample were weighed out and placed on a black plastic sheet. 4to 5 drops at a time of boiling linseed oil contained in a biuret weredropped onto the sample from above and adequately kneaded with thepowder using a spatula at the time of each addition. Once the entiremixture become a clump in the form of a hard pate, the boiling linseedoil was kneaded one drop at a time, dropping was ended immediatelybefore the mixture suddenly became soft with the addition of a singledrop, and the amount of boiling linseed oil dropped onto the sample atthat time was read followed by calculation of oil absorption accordingto the equation indicated below.

Oil absorption (mL/g)=Volume of boiling linseed oil dropped onto sample(mL)/sample weight (g)

Test Example 2

Each of the samples of the above-mentioned examples and comparativeexamples were investigated for the relationship between aluminum contentand bulk specific volume or oil absorption.

The results are shown in FIG. 2. As is clear from the results of FIG. 2,in the case of having added an aluminum component, both bulk specificvolume and oil absorption were found to increase in comparison with thecase of an aluminum content of 0.0058% by weight.

In particular, that effect was found to be able to be demonstrated evenat a comparatively small amount of aluminum component of 0.10% by weightto 0.60% by weight.

Test Example 3

Bulk specific volume and oil absorption were investigated for a sample(sample no. 9) prepared in the same manner as sample no. 5 of Example 1with the exception of changing the conditions of hydrothermal treatmentto 4 hours at 200° C. The results are shown in FIG. 3. Results for asample to which an aluminum component was not added (sample no. 8) arealso shown in FIG. 3. As is clear from the results of FIG. 3, a samplehaving an aluminum content of 0.23% by weight was found to demonstratehigher levels of bulk specific volume and oil absorption than a sampleto which an aluminum component was not added.

Test Example 4

Values for pH, mean particle diameter, aluminum content and specificsurface area and the like were investigated for the above-mentionedsample nos. 5 and 9. The results are shown in Table 2. Measurementresults for samples to which an aluminum component was not added (samplenos. 1 and 8) are also shown in Table 2.

TABLE 2 No. 1 No. 8 No. 5 No. 9 Hydrothermal 200 200 200 200 treatmenttemp. (° C.) Hydrothermal 3 4 3 4 treatment time (h) pH (5%) 9.18 8.799.19 9.01 Bulk (mL/g) 7.35 8.6 15.39 14.3 Oil 2.5 4.6 3.6 5.0 absorption(mL/g) Specific 53.8 118.6 133.1 171.2 surface area (m²/g) Mean 20.940.2 20.6 29.7 particle diameter (μm) Al (%) 0.0058 0.01 0.38 0.23

As is clear from the results of Table 2, sample nos. 5 and 9 were foundto demonstrate higher levels of bulk specific volume and oil absorptionthan the samples to which an aluminum component was not added, andspecific surface area was also determined to be comparatively highwithin the range of 120 m²/g to 180 m²/g.

1.-6. (canceled)
 7. A calcium silicate-based material containing an aluminum component, the calcium silicate-based material having: (1) a bulk specific volume of 8 mL/g or more and an oil absorption of 2.5 mL/g or more; and (2) an aluminum content of 0.1% by weight to 1.0% by weight.
 8. The calcium silicate-based material according to claim 7, which contains gyrolite calcium silicate crystals.
 9. The calcium silicate-based material according to claim 7, wherein the specific surface area is 120 m²/g or more.
 10. A pharmaceutical composition comprising the calcium silicate-based material according to claim
 7. 